Energy-efficient recovery of fermented butyric acid using octyl acetate extraction.

Biofuel Butyric acid recovery Energy-efficient Solvent extraction

Journal

Biotechnology for biofuels and bioproducts
ISSN: 2731-3654
Titre abrégé: Biotechnol Biofuels Bioprod
Pays: England
ID NLM: 9918300888906676

Informations de publication

Date de publication:
06 May 2022
Historique:
received: 12 12 2021
accepted: 22 04 2022
entrez: 6 5 2022
pubmed: 7 5 2022
medline: 7 5 2022
Statut: epublish

Résumé

A butyric acid recovery process using octyl acetate is proposed, and the design details of the extraction and subsequent distillation processes were investigated. Ternary equilibrium data for the extractor design were derived from molecular simulations and experimental measurements. A new procedure for estimating the thermodynamic parameters was introduced to determine the effect of the parameters on extractor design by comparison with previously reported parameters. Using the proposed recovery process with the newly estimated thermodynamic model, 99.8% butyric acid was recovered from the fermentation broth at a recovery rate of 99%. The energy demand for the proposed process was found to be lower than the average demand for several reported butyric acid recovery processes. The investment cost is projected to be lower than that of other butyric acid processes due to the high efficiency of extraction solvent. The recovery cost of butyric acid was comparable to its selling price.

Sections du résumé

BACKGROUND BACKGROUND
A butyric acid recovery process using octyl acetate is proposed, and the design details of the extraction and subsequent distillation processes were investigated. Ternary equilibrium data for the extractor design were derived from molecular simulations and experimental measurements.
RESULTS RESULTS
A new procedure for estimating the thermodynamic parameters was introduced to determine the effect of the parameters on extractor design by comparison with previously reported parameters. Using the proposed recovery process with the newly estimated thermodynamic model, 99.8% butyric acid was recovered from the fermentation broth at a recovery rate of 99%. The energy demand for the proposed process was found to be lower than the average demand for several reported butyric acid recovery processes.
CONCLUSIONS CONCLUSIONS
The investment cost is projected to be lower than that of other butyric acid processes due to the high efficiency of extraction solvent. The recovery cost of butyric acid was comparable to its selling price.

Identifiants

pubmed: 35524283
doi: 10.1186/s13068-022-02146-6
pii: 10.1186/s13068-022-02146-6
pmc: PMC9074251
doi:

Types de publication

Journal Article

Langues

eng

Pagination

46

Subventions

Organisme : National Research Foundation of Korea
ID : 2021R1A2C209425611
Organisme : Korea Institute of Energy Technology Evaluation and Planning
ID : 20194010201840

Informations de copyright

© 2022. The Author(s).

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Auteurs

Hyeon Woo Oh (HW)

Department of Chemical Engineering, Pukyong National University, 365 Shinsun-ro, Nam-gu, Busan, 48547, South Korea.

Seong Chan Lee (SC)

Department of Chemical Engineering, Pukyong National University, 365 Shinsun-ro, Nam-gu, Busan, 48547, South Korea.

Hee Chul Woo (HC)

Department of Chemical Engineering, Pukyong National University, 365 Shinsun-ro, Nam-gu, Busan, 48547, South Korea. woohc@pknu.ac.kr.

Young Han Kim (YH)

Department of Chemical Engineering, Pukyong National University, 365 Shinsun-ro, Nam-gu, Busan, 48547, South Korea. yhkim2@pknu.ac.kr.

Classifications MeSH